MY117027A - Polymerization process using separated flow. - Google Patents

Polymerization process using separated flow.

Info

Publication number
MY117027A
MY117027A MYPI97006067A MYPI9706067A MY117027A MY 117027 A MY117027 A MY 117027A MY PI97006067 A MYPI97006067 A MY PI97006067A MY PI9706067 A MYPI9706067 A MY PI9706067A MY 117027 A MY117027 A MY 117027A
Authority
MY
Malaysia
Prior art keywords
raw material
reactor
gas
liquid phase
phase
Prior art date
Application number
MYPI97006067A
Other languages
English (en)
Inventor
Akihiro Sakamoto
Shunyou Uesugi
Original Assignee
Mitsui Chemicals Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsui Chemicals Inc filed Critical Mitsui Chemicals Inc
Publication of MY117027A publication Critical patent/MY117027A/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F10/02—Ethene
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006—Controlling or regulating processes
    • B01J19/0013—Controlling the temperature of the process
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2415—Tubular reactors
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/04—Pressure vessels, e.g. autoclaves
    • B01J3/042—Pressure vessels, e.g. autoclaves in the form of a tube
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/16—Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00094—Jackets

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Polymerisation Methods In General (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
MYPI97006067A 1996-12-26 1997-12-16 Polymerization process using separated flow. MY117027A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP34819596 1996-12-26
JP25703697A JP3836228B2 (ja) 1996-12-26 1997-09-22 分離流による重合方法

Publications (1)

Publication Number Publication Date
MY117027A true MY117027A (en) 2004-04-30

Family

ID=26543025

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI97006067A MY117027A (en) 1996-12-26 1997-12-16 Polymerization process using separated flow.

Country Status (10)

Country Link
US (1) US6111035A (fr)
EP (1) EP0850962B1 (fr)
JP (1) JP3836228B2 (fr)
KR (1) KR19980064551A (fr)
CN (1) CN1218968C (fr)
CA (1) CA2225639A1 (fr)
DE (1) DE69707826T2 (fr)
ID (1) ID19349A (fr)
MY (1) MY117027A (fr)
TW (1) TW442499B (fr)

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1453883B1 (fr) * 2000-12-07 2012-11-21 Grupo Petrotemex, S.A. de C.V. Procede de preparation de polyester a faible cout mettant en oeuvre un reacteur tubulaire
US6906164B2 (en) 2000-12-07 2005-06-14 Eastman Chemical Company Polyester process using a pipe reactor
US7135541B2 (en) * 2003-06-06 2006-11-14 Eastman Chemical Company Polyester process using a pipe reactor
US7943094B2 (en) 2006-12-07 2011-05-17 Grupo Petrotemex, S.A. De C.V. Polyester production system employing horizontally elongated esterification vessel
US7649109B2 (en) 2006-12-07 2010-01-19 Eastman Chemical Company Polyester production system employing recirculation of hot alcohol to esterification zone
US7863477B2 (en) 2007-03-08 2011-01-04 Eastman Chemical Company Polyester production system employing hot paste to esterification zone
US7872090B2 (en) 2007-07-12 2011-01-18 Eastman Chemical Company Reactor system with optimized heating and phase separation
US7872089B2 (en) 2007-07-12 2011-01-18 Eastman Chemical Company Multi-level tubular reactor with internal tray
US7847053B2 (en) 2007-07-12 2010-12-07 Eastman Chemical Company Multi-level tubular reactor with oppositely extending segments
US7829653B2 (en) 2007-07-12 2010-11-09 Eastman Chemical Company Horizontal trayed reactor
US7868130B2 (en) 2007-07-12 2011-01-11 Eastman Chemical Company Multi-level tubular reactor with vertically spaced segments
US7842777B2 (en) 2007-07-12 2010-11-30 Eastman Chemical Company Sloped tubular reactor with divided flow
US7858730B2 (en) 2007-07-12 2010-12-28 Eastman Chemical Company Multi-level tubular reactor with dual headers
US7868129B2 (en) 2007-07-12 2011-01-11 Eastman Chemical Company Sloped tubular reactor with spaced sequential trays
WO2009045382A1 (fr) * 2007-10-04 2009-04-09 Merck & Co., Inc. Dérivé d'arylsulfone substituée comme bloqueurs des canaux calciques
US20100113692A1 (en) * 2008-11-04 2010-05-06 Mcguire Jr James E Apparatus for Continuous Production of Partially Polymerized Compositions
CN101928197A (zh) * 2009-06-26 2010-12-29 中国石油化工股份有限公司 热二聚环戊二烯的方法
KR100999555B1 (ko) * 2010-07-09 2010-12-08 대림산업 주식회사 삼상 유동층 반응기를 이용한 알파-올레핀의 삼상중합 방법
JP5888722B2 (ja) * 2010-08-23 2016-03-22 株式会社明治 飲食品のオーバーランのインライン連続測定方法及び測定装置、並びに、当該測定方法を使用した飲食品の製造方法と、これにより製造した飲食品
CN103333278B (zh) * 2013-01-30 2016-02-24 衢州市鼎盛化工科技有限公司 一种制备含氟聚合物和含氟共聚物的装置及其工艺
CN103446990B (zh) * 2013-08-29 2015-12-23 中国化学赛鼎宁波工程有限公司 切向环流管式非均相反应器
EP3088388A1 (fr) 2015-04-30 2016-11-02 NicOx S.A. Dérivés de prostaglandines donneurs d'oxyde nitrique

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1620941A1 (de) * 1966-11-26 1970-05-14 Imhico Ag Verfahren zur Herstellung von Polyaethylen
US4133944A (en) * 1973-03-29 1979-01-09 Imperial Chemical Industries Limited Ethylene polymerization
US4089888A (en) * 1976-07-12 1978-05-16 Idemitsu Petrochemical Co. Ltd. Method for producing a polycarbonate oligomer
FR2385745A1 (fr) * 1977-03-31 1978-10-27 Charbonnages Ste Chimique Procede de polymerisation de l'ethylene, sous pressions elevees, avec recyclage
DE2719967A1 (de) * 1977-05-04 1978-11-09 Bayer Ag Kontinuierliches verfahren zur durchfuehrung von stofftransportbedingten reaktionen
DE3066423D1 (en) * 1979-11-06 1984-03-08 Ube Industries Process for polymerizing formaldehyde
US5243005A (en) * 1988-09-07 1993-09-07 Mitsui Petrochemical Industries, Ltd. Process for producing cycloolefin random copolymers
FR2659338B1 (fr) * 1990-03-09 1993-05-07 Bp Chemicals Snc Procedes et dispositifs de polymerisation catalytique d'alpha-olefines en phase gazeuse.
US5589555A (en) * 1991-10-03 1996-12-31 Novacor Chemicals (International) S.A. Control of a solution process for polymerization of ethylene
US5644007A (en) * 1996-04-26 1997-07-01 Minnesota Mining And Manufacturing Company Continuous process for the production of poly(1-alkenes)
US5859157A (en) * 1996-10-16 1999-01-12 Equistar Chemicals, Lp Process for gas phase polymerization of olefins

Also Published As

Publication number Publication date
EP0850962A3 (fr) 1998-07-08
KR19980064551A (ko) 1998-10-07
EP0850962A2 (fr) 1998-07-01
JP3836228B2 (ja) 2006-10-25
US6111035A (en) 2000-08-29
JPH10237112A (ja) 1998-09-08
CN1218968C (zh) 2005-09-14
TW442499B (en) 2001-06-23
ID19349A (id) 1998-07-02
CN1186077A (zh) 1998-07-01
DE69707826T2 (de) 2002-04-11
CA2225639A1 (fr) 1998-06-26
DE69707826D1 (de) 2001-12-06
EP0850962B1 (fr) 2001-10-31

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